CN205892941U - High -efficient emergent safe water treatment facility - Google Patents
High -efficient emergent safe water treatment facility Download PDFInfo
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- CN205892941U CN205892941U CN201620865478.5U CN201620865478U CN205892941U CN 205892941 U CN205892941 U CN 205892941U CN 201620865478 U CN201620865478 U CN 201620865478U CN 205892941 U CN205892941 U CN 205892941U
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Abstract
The utility model discloses a high -efficient emergent safe water treatment facility, including the system of intaking, dense media flocculation and precipitation system, ultrafiltration system, active carbon adsorption filtration system and disinfection system, the system of intaking includes raw water intake pump and static mixer, dense media flocculation and precipitation system includes dense media flocculation reaction tank, heavy medium recovery device and parallel tubes sedimentation tank, the ultrafiltration system includes membrane cisterna, milipore filter subassembly and backwash water tank, the ultrafiltration system includes membrane cisterna, milipore filter subassembly and backwash water tank, active carbon adsorption filtration system includes an active carbon filtration post, the disinfection system is including disinfection water tank and disinfectant case. The utility model has the advantages of: high -efficient emergent safe water treatment facility investment is little, simple to operate, strong adaptability, and complete equipment can realize full automatic operation, produces water security, maintains simple and conveniently that it is efficient to produce water, can realize quick large -traffic water supply.
Description
Technical field
This utility model is related to a kind of emergent technical field of water treatment equipment, at the efficiently emergent safe water of one kind
Reason equipment.
Background technology
Make rapid progress in mankind's science and technology, under the background that urbanization paces are gradually accelerated, water-supply systems are also faced with many
Challenge again.It is that product water water supply accident species is increasing first.Water system is not only faced with earthquake, big flood, landslide, mud
The impact of the Nature weather such as rock glacier, is also subjected to biology, chemistry, the material such as virus, greasy dirt produced by mankind's activity
Pollution.Secondly frequency produced by accident is also increasing.Bread is the staff of life, food with water as elder generation, have stable, safe,
Clean drinking water, is the primary demand of human survival and the necessary guarantee of health, be also lift oneself out of poverty, promote social harmony,
Realize the important foundation of sustainable development.
In addition, restricted by nature, the condition such as economic and social, in scarcely populated, with a varied topography, sparsely populated rural area
Area, temporarily unconditional construction concentrates water supply project in flakes or uneconomical, China's Rural water supply of building central water supply engineering
, based on traditional, backward, small-sized, dispersion, simple and crude water facilities, tap water popularity rate is low for facility, and DRINKING WATER is difficult and pacifies
Full problem long-term existence.For field work units such as large-scale petroleum exploration, water resources and hydropower construction, railways, directly take earth's surface
Water or subsoil water all cannot ensure that workmen's is healthy.
Accordingly, it is desirable to provide one kind is efficiently met an urgent need, safe water treatment facilities are solving the above problems.
Utility model content
The technical problems to be solved in the utility model be provide a kind of can solve the problem that produce water efficiency low, produce water unwell complete height
Effect suddenly safe water treatment facilities.
For solving above-mentioned technical problem, the technical solution of the utility model is: one kind is efficiently met an urgent need safe water treatment facilities,
Its innovative point is: includes water inlet system, dense media flocculation sedimentation system, ultrafiltration system, activated carbon adsorption filtration system and disappears
Malicious system；
Described water inlet system includes raw water intake pump and static mixer, and described raw water intake pump is arranged at water source, institute
State raw water to connect by raw water intake pump to the water inlet of static mixer, described water inlet system also includes explosive box a and dosing
Pump a, described explosive box a is connected to static mixer by dosing pump a；
Described dense media flocculation sedimentation system includes dense media flocculation tank, dense media retracting device and parallel pipe precipitation
Pond, the described water inlet of dense media flocculation tank is connected with the outlet of static mixer, described static mixer and dense medium
It is provided with effusion meter a, the outlet of described dense media flocculation tank connects to parallel pipe sedimentation tank between matter flocculation tank,
The mud mouth of described parallel pipe sedimentation tank lower end is connected to dense media retracting device by sludge reflux pump, and described dense media reclaims
Device connects dense media flocculation tank, and described dense media flocculation tank includes primary flocculation basin, flocculation basin and aerobic fermentation tank, often
It is provided with blender, described primary flocculation basin, flocculation basin and aerobic fermentation tank set successively according to after water (flow) direction the past in individual pond
Put, described dense media retracting device includes dense media powder flco cracking flossing machine and dense media powder seperator, described parallel pipe sedimentation tank
The mud mouth of lower end is connected to flocculation basin by a sludge reflux pump part, and another part connects dense media powder flco cracking flossing machine extremely
Dense media powder seperator, described dense media powder seperator connects to primary flocculation basin, between described sludge reflux pump and flocculation basin
It is provided with effusion meter b, between described sludge reflux pump and dense media powder flco cracking flossing machine, be provided with effusion meter c, described dense media
Flocculation sedimentation system also includes explosive box b and dosing pump b, and described explosive box b is connected with flocculation basin by dosing pump b；
Described ultrafiltration system includes membrane cisterna, hyperfiltration membrane assembly and backwash water tank, and described membrane cisterna is connected with parallel pipe sedimentation tank
Connect, described hyperfiltration membrane assembly is arranged in membrane cisterna, the bottom of described membrane cisterna is connected with aerating system by aeration tube, described activity
Charcoal adsorption filtration system includes an activated carbon column, and described activated carbon column is connected with membrane cisterna by suction pump, described suction
It is provided with effusion meter d, described backwash water tank is arranged between effusion meter d and activated carbon column, institute between pump and activated carbon column
State backwash water tank to connect to membrane cisterna by backwash water pump；
Described decontamination system includes Sterilizing water tank and disinfectant box, and described Sterilizing water tank connects to activated carbon column, described
Disinfectant box is respectively connecting to static mixer and Sterilizing water tank by disinfectant pump.
Further, the upper end of described primary flocculation basin offers benefit dense media powder mouth.
Further, described aerating system is aeration blower.
Further, described all processing equipments, pipeline and instrumentation are arranged in standard-sized container.
Further, described container is dry cargo container, and described all processing equipments, pipeline and instrumentation are integrated
For modularized equipment and be arranged in dry cargo container.
The utility model has the advantage of:
(1) this utility model increased activated carbon column and carries out adsorbing, filters, activated carbon to abnormal flavour in water body, Organic substance,
Colloid, heavy metal ion, chlorine residue, turbidity, colourity etc. have good absorption and filtration, improve the safety producing water.
(2) this utility model adopts dense media powder to participate in coagulating sedimentation, (micro- to add micron order inertia high density microparticle
Sand or magnetite powder) as flocculation core, thus forming the compound flco with high concentration and big density feature, make flco form speed
Degree and settling velocity are greatly improved, and raw water is purified in very short time.
(3) this utility model adopts parallel pipe sedimentation tank, and parallel pipe sedimentation tank is that a kind of water channel is respectively provided with muddy road
New sedimentation tank, the tube settler uniting two into one compared to water channel and muddy road, its deposition efficiency is higher, and settling velocity is faster.
(4) can quick big flow quality classification water supply, output water includes drinking water and daily water consumption, and drinking water is available for directly drinking
With daily water consumption is available for the daily life water in addition to directly drinking.
(5) upper end of primary flocculation basin offers benefit dense media powder mouth, when in course of reaction, dense media powder is inadequate, permissible
By mending dense media powder mouth, add dense media powder into primary flocculation basin.
(6) aerating system be aeration blower, enough pressure can be produced, make oxygen be sufficiently stirred in a liquid with molten
Solution.
(7) all processing equipments, pipeline and instrumentation are arranged in standard-sized container, and container is dried food and nuts
Container, all processing equipments, pipeline and instrumentation are integrated into modularized equipment, small volume, convenient transportation.
Brief description
With reference to the accompanying drawings and detailed description this utility model is described in further detail.
Fig. 1 is a kind of system block diagram of safe water treatment facilities of efficiently meeting an urgent need of this utility model.
Fig. 2 is a kind of structural representation of safe water treatment facilities of efficiently meeting an urgent need of this utility model.
Fig. 3 is a kind of arrangement schematic diagram of safe water treatment facilities of efficiently meeting an urgent need of this utility model.
Specific embodiment
The following examples can make professional and technical personnel that this utility model is more fully understood, but therefore will not
This utility model is limited among described scope of embodiments.
The safe water treatment facilities as shown in figure 1, one kind is efficiently met an urgent need, including water inlet system, dense media flocculation sedimentation system,
Ultrafiltration system, activated carbon adsorption filtration system and decontamination system.
As shown in Figure 2 to Figure 3, water inlet system includes raw water intake pump 1 and static mixer 2, and raw water intake pump 1 is arranged on
At water source, raw water is connected to the water inlet of static mixer 2 by raw water intake pump 1, water inlet system also include explosive box a10 and
Dosing pump a11, explosive box a10 is connected to static mixer 2 by dosing pump a11.
Dense media flocculation sedimentation system includes dense media flocculation tank, dense media retracting device and parallel pipe sedimentation tank
14, the water inlet of dense media flocculation tank is connected with the outlet of static mixer 2, and static mixer 2 is flocculated with dense media
It is provided with effusion meter a3, the outlet of dense media flocculation tank connects to parallel pipe sedimentation tank 14, parallel pipe between reaction tank
The mud mouth of sedimentation tank 14 lower end is connected to dense media retracting device by sludge reflux pump 15, and dense media retracting device connects weight
Medium flocculation tank.
In dense media flocculation tank, dense media powder participates in coagulating sedimentation, to add micro- of micron order inertia high density
Grain (micro- sand or magnetite powder), as flocculation core, thus forming the compound flco with high concentration and big density feature, makes flco
Form speed and settling velocity is greatly improved, raw water is purified in very short time, parallel pipe sedimentation tank 14 is a kind of
The new sedimentation tank that water channel and muddy road are respectively provided with, the tube settler uniting two into one compared to water channel and muddy road, its precipitation effect
Rate is higher, and settling velocity faster, therefore produces water efficiency high.
Dense media flocculation tank includes primary flocculation basin 4, flocculation basin 6 and aerobic fermentation tank 8, is provided with primary flocculation basin 4
Blender a5, is provided with blender b7 in flocculation basin 6, be provided with blender c9, primary flocculation basin 4, flocculation basin 6 in aerobic fermentation tank 8
Set gradually according to after water (flow) direction the past with aerobic fermentation tank 8.
Dense media retracting device includes dense media powder flco cracking flossing machine 18 and dense media powder seperator 19, parallel pipe sedimentation tank
The mud mouth of 14 lower ends is connected to flocculation basin 6 by sludge reflux pump 15 part, and another part connects dense media powder flco solution
To dense media powder seperator 19, dense media powder seperator 19 connects to primary flocculation basin 4, the upper end of primary flocculation basin 4 wadding machine 18
Offer benefit dense media powder mouth 20, between sludge reflux pump 15 and flocculation basin 6, be provided with effusion meter b16, sludge reflux pump 15 with
It is provided with effusion meter c17, dense media flocculation sedimentation system also includes explosive box b12 and adds between dense media powder flco cracking flossing machine 18
Teat pipette b13, explosive box b12 are connected with flocculation basin 6 by dosing pump b13.
Ultrafiltration system includes membrane cisterna 21, hyperfiltration membrane assembly 22 and backwash water tank 27, membrane cisterna 21 and parallel pipe sedimentation tank 14 phase
Connect, hyperfiltration membrane assembly 22 is arranged in membrane cisterna 21, and the bottom of membrane cisterna 21 is connected with aeration blower 23 by aeration tube, can
Produce enough pressure, play well-beaten effect.
Activated carbon adsorption filtration system includes an activated carbon column 29, activated carbon to abnormal flavour in water body, Organic substance, colloid,
Heavy metal ion, chlorine residue, turbidity, colourity etc. have good absorption and filtration, improve the safety producing water.
Activated carbon column 29 is connected with membrane cisterna 21 by suction pump 24, arranges between suction pump 24 and activated carbon column 29
Have effusion meter d26, between suction pump 24 and effusion meter d26, be provided with pressure gauge 25, backwash water tank 27 be arranged on effusion meter d26 with
Between activated carbon column 29, backwash water tank 27 is connected to membrane cisterna 21 by backwash water pump 28.
Decontamination system includes Sterilizing water tank 30 and disinfectant box 31, and Sterilizing water tank 30 connects to activated carbon column 29, sterilizes
Agent case 31 is respectively connecting to static mixer 2 and Sterilizing water tank 30 by disinfectant pump 32.
All processing equipments, pipeline and instrumentation are arranged in standard-sized container, and container is dried food and nuts collection
Vanning, all processing equipments, pipeline and instrumentation are integrated into modularized equipment, small volume, convenient transportation.
During using this efficiently emergent safe water treatment facilities, specifically comprise the following steps that (1) intakes: the raw water warp at water source
Raw water intake pump 1 enters static mixer 2, and the aluminium polychlorid in explosive box a10 throws static mixer into by dosing pump a11
2, realize being sufficiently mixed through static mixer 2；(2) dense media flocculation sediment: the polyacrylamide in explosive box b12 passes through dosing
Pump b13 throws in flocculation basin 6, and the mixed liquor of coagulant and raw water is sequentially entered primary flocculation basin 4, flocculation basin 6, ripe in order
Change in pond 8, mixing flow quantity measures through effusion meter a3, respectively in blender a5, blender b7, the stirring action of blender c9
Under, carry out flocculation reaction, form the alumen ustum containing dense media powder, enter back in parallel pipe sedimentation tank 14, big containing in water
Grain material and partial solubility Organic substance are attached to and precipitate on alumen ustum, and are flowed back by sludge reflux pump 15, backflow
Matter sludge containing dense medium a part be passed straight back in flocculation basin 6 by pipeline, participate in flocculation reaction, returned sludge flow through flow
Gauge b16 measures, and some carries out entering dense media powder after flco solution wadding separates by dense media powder flco cracking flossing machine 18
Seperator 19 reclaims dense media powder, mud discharging, and the dense media powder of recovery enters in primary flocculation basin 4 and participates in flocculation reaction, shape
Become circulation, reclaim mud discharge and measure through effusion meter c17, the supernatant of parallel pipe sedimentation tank 14 can be commonly used directly as day
Water；(3) ultrafiltration membrance filter: the supernatant in parallel pipe sedimentation tank 14 is entered membrane cisterna 21, the ultrafilter membrane in membrane cisterna 21
Assembly 22 filter bacteria and virus, in ultra-filtration process, carry out air purge by aeration blower 23, membrane cisterna 21 timing is by backwash water pump 28
Draw water from backwash water tank 27 and carry out backwash, to ensure effectively carrying out of filtration；(4) activated carbon adsorption: membrane cisterna 21 is in suction
Water outlet in the presence of pump 24, water outlet, after effusion meter d26 metering, is squeezed into activated carbon column 29, is carried out activated carbon adsorption；(5) disappear
Poison: enter Sterilizing water tank 30 after activated carbon column 29 adsorption filtration and carry out disinfection, the disinfectant in disinfectant box 31 is passed through to disappear
Toxic agent pump 32 squeezes into Sterilizing water tank 30 and static mixer 2, carries out front sterilization and rear sterilization, and front sterilization adds in raw water intake pump
After 1 and before static mixer 2, for the situation more than summer raw water algae, afterwards sterilization add after activated carbon column 29 and
Before Sterilizing water tank 30, the water in Sterilizing water tank 30 can provide domestic water after disinfecting.
Of the present utility model ultimate principle and principal character have been shown and described above.The technical staff of the industry should
Solution, this utility model is not restricted to the described embodiments, and this practicality is new for simply illustrating described in above-described embodiment and description
The principle of type, on the premise of without departing from this utility model spirit and scope, this utility model also has various changes and modifications,
These changes and improvements both fall within the range of claimed this utility model.This utility model claims scope by appended
Claims and its equivalent thereof.
Claims (5)
1. one kind efficiently meet an urgent need safe water treatment facilities it is characterised in that: include water inlet system, dense media flocculation sedimentation system,
Ultrafiltration system, activated carbon adsorption filtration system and decontamination system；
Described water inlet system includes raw water intake pump and static mixer, and described raw water intake pump is arranged at water source, described former
Water is connected by raw water intake pump to the water inlet of static mixer, and described water inlet system also includes explosive box a and dosing pump a,
Described explosive box a is connected to static mixer by dosing pump a；
Described dense media flocculation sedimentation system includes dense media flocculation tank, dense media retracting device and parallel pipe sedimentation tank,
The described water inlet of dense media flocculation tank is connected with the outlet of static mixer, and described static mixer is wadded a quilt with cotton with dense media
It is provided with effusion meter a, the outlet of described dense media flocculation tank connects to parallel pipe sedimentation tank, described between solidifying reaction tank
The mud mouth of parallel pipe sedimentation tank lower end is connected to dense media retracting device, described dense media retracting device by sludge reflux pump
Connect dense media flocculation tank, described dense media flocculation tank includes primary flocculation basin, flocculation basin and aerobic fermentation tank, each pond
Inside it is provided with blender, described primary flocculation basin, flocculation basin and aerobic fermentation tank set gradually according to after water (flow) direction the past, institute
State dense media retracting device and include dense media powder flco cracking flossing machine and dense media powder seperator, described parallel pipe sedimentation tank lower end
Mud mouth is connected to flocculation basin by a sludge reflux pump part, and another part connects dense media powder flco cracking flossing machine to dense media
Powder seperator, described dense media powder seperator connects to primary flocculation basin, is provided between described sludge reflux pump and flocculation basin
Effusion meter b, is provided with effusion meter c between described sludge reflux pump and dense media powder flco cracking flossing machine, described dense media flocculation is heavy
Shallow lake system also includes explosive box b and dosing pump b, and described explosive box b is connected with flocculation basin by dosing pump b；
Described ultrafiltration system includes membrane cisterna, hyperfiltration membrane assembly and backwash water tank, and described membrane cisterna is connected with parallel pipe sedimentation tank, institute
State hyperfiltration membrane assembly to be arranged in membrane cisterna, the bottom of described membrane cisterna is connected with aerating system by aeration tube, described activated carbon is inhaled
Attached filtration system includes an activated carbon column, and described activated carbon column is connected with membrane cisterna by suction pump, described suction pump with
It is provided with effusion meter d, described backwash water tank is arranged between effusion meter d and activated carbon column between activated carbon column, described anti-
Water tank is connected to membrane cisterna by backwash water pump；
Described decontamination system includes Sterilizing water tank and disinfectant box, and described Sterilizing water tank connects to activated carbon column, described sterilization
Agent case is respectively connecting to static mixer and Sterilizing water tank by disinfectant pump.
2. one kind according to claim 1 efficiently meet an urgent need safe water treatment facilities it is characterised in that: described primary flocculation basin
Upper end offer benefit dense media powder mouth.
3. one kind according to claim 1 efficiently meet an urgent need safe water treatment facilities it is characterised in that: described aerating system is
Aeration blower.
4. one kind according to claim 1 efficiently meet an urgent need safe water treatment facilities it is characterised in that: described all process
Equipment, pipeline and instrumentation are arranged in standard-sized container.
5. one kind according to claim 1 efficiently meet an urgent need safe water treatment facilities it is characterised in that: described container is dry
Goods container, described all processing equipments, pipeline and instrumentation are integrated into modularized equipment and are arranged on dry cargo container
Interior.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620865478.5U CN205892941U (en) | 2016-08-11 | 2016-08-11 | High -efficient emergent safe water treatment facility |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620865478.5U CN205892941U (en) | 2016-08-11 | 2016-08-11 | High -efficient emergent safe water treatment facility |
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| CN205892941U true CN205892941U (en) | 2017-01-18 |
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| CN201620865478.5U Active CN205892941U (en) | 2016-08-11 | 2016-08-11 | High -efficient emergent safe water treatment facility |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114133062A (en) * | 2021-11-23 | 2022-03-04 | 天津市融泰水务有限公司 | Water treatment device for surface water purification and application |
-
2016
- 2016-08-11 CN CN201620865478.5U patent/CN205892941U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114133062A (en) * | 2021-11-23 | 2022-03-04 | 天津市融泰水务有限公司 | Water treatment device for surface water purification and application |
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Effective date of registration: 20191008 Granted publication date: 20170118 |
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Date of cancellation: 20221008 Granted publication date: 20170118 |
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